| Literature DB >> 25617619 |
Xueqin Lu1, Guangyin Zhen2, Adriana Ledezma Estrada3, Mo Chen4, Jialing Ni3, Toshimasa Hojo3, Kengo Kubota3, Yu-You Li5.
Abstract
Long-term performance of a lab-scale UASB reactor treating starch wastewater was investigated under different hydraulic retention times (HRT). Successful start-up could be achieved after 15days' operation. The optimal HRT was 6h with organic loading rate (OLR) 4g COD/Ld at COD concentration 1000mg/L, attaining 81.1-98.7% total COD removal with methane production rate of 0.33L CH4/g CODremoved. Specific methane activity tests demonstrated that methane formation via H2-CO2 and acetate were the principal degradation pathways. Vertical characterizations revealed that main reactions including starch hydrolysis, acidification and methanogenesis occurred at the lower part of reactor ("main reaction zone"); comparatively, at the up converting acetate into methane predominated ("substrate-shortage zone"). Further reducing HRT to 3h caused volatile fatty acids accumulation, sludge floating and performance deterioration. Sludge floating was ascribed to the excess polysaccharides in extracellular polymeric substances (EPS). More efforts are required to overcome sludge floating-related issues.Entities:
Keywords: Extracellular polymeric substances (EPS); Granular sludge; Methane; Starch; Upflow anaerobic sludge blanket (UASB)
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Year: 2015 PMID: 25617619 DOI: 10.1016/j.biortech.2015.01.010
Source DB: PubMed Journal: Bioresour Technol ISSN: 0960-8524 Impact factor: 9.642